TECHNICAL FIELD
[0001] This invention relates to an in-mold coating composition and an in-mold-coated molded
product, and more particularly to an in-mold-coated molded product obtained by a so-called
in-mold coating molding method (which is also referred to as an IMC method or an in-mold
coating method) in which a thermoplastic molding material or a thermosetting plastic
molding material is molded in a mold by means of an injection molding method, an injection
compression molding method, an injection press molding method, a compression molding
method or a reaction injection molding method, and then an in-mold coating composition
is injected between the surface of the obtained molded product and the surface of
a mold cavity and cured in the mold to produce an integral molded product in which
the in-mold coating composition adheres to the surface of the molded plastic product.
BACKGROUND ART
[0002] For the purpose of lengthening a life of product by improving a scratch resistance
in the surface of a molded plastic product used for automobiles, construction machines,
architectural materials or the like, or improving a weathering resistance, coating
a molded product has been heretofore used widely. In this case, an electrostatic coating
is generally used for improving a coating efficiency in top coating or reducing the
emission of volatile organic compounds (VOC) to the atmosphere. However, the volume
resistivity value of molded plastic product is usually 10
10 Ω/cm
2 or more, and hence it is difficult to coating uniformly with a coating material even
if the electrostatic coating method is used. Thus, when these molded products are
subjected to the electrostatic coating, a spray coating with a conductive primer coating
material is carried out for the purpose of forming a coating film having conductive
properties. However, there is recently a strong interest about environmental issues,
and the tendency to limit severely the emission of volatile organic compounds, what
is called VOC, from paint factories to the atmosphere becomes stronger, and thus the
development of an alternative technique to the conventional conductive primer is imperative.
[0003] Under such a situation, an in-mold coating molding method of injecting a coating
material between the surface of a molded plastic product formed in a mold and the
cavity surface of the mold, and thereafter curing the coating material in the mold
to produce an integral molded product in which a coating film adheres to the surface
of the molded plastic product attracts attention.
Since the in-mold coating molding method forms a coating film in a mold, the coating
composition comprises no solvent and 100% coating film is formed in the mold. Thus,
such a method emits no VOC into the atmosphere, and generates less waste, and has
less impact on the environment. Also, the coating film is cured with a radical reaction
by the heat of a mold, the heat of a thermoplastic resin in resin-plasticizing, and
the heat of reaction of a thermosetting resin, and hence the expenditure of energy
in forming of the coating film is lower as compared with reaction through the heat
of a general drying furnace or ultraviolet irradiation. It is, therefore, said to
be an excellent coating method.
[0004] The coating material used for in-mold coating molding is required to be cured for
a short time with no solvents because of forming a coating film in a mold. Thus, the
development is more difficult than that of general coating materials. In an already-developed
conductive coating material used for an in-mold coating molding method, carbon black
is used as a conductive material (for example, see Patent Documents 1 and 2).
[0005] Recently, design or color tone is emphasized, and thereby a coating material for
in-mold coating molding having conductive properties and light color is required for
the coating color of top coating material, and specifically for a light-colored metallic
or pearl coating material. For such purpose, graphite is mainly used as a conductive
material and titanium dioxide is contained as a coloring pigment for light color.
The cured coating film takes on gray, but has insufficient whiteness degree and brightness
if coated with a white color-based coating material having a poor hiding power and
high brightness in top coating (for example, see Patent Document 3).
[0006] On the other hand, coating materials containing an organic solvent are generally
used as a white conductive coating material (for example, see Patent Documents 4-8).
However, they emits a large amount of VOC to the atmosphere in coating as mentioned
above, and thus the development of coating materials of non-solvent type is demanded
from the viewpoint of dealing with recent environment issues.
CITED DOCUMENTS LIST
PATENT DOCUMENT
SUMMARY OF THE INVENTION
PROBLEMS TO BE SOLVED BY THE INVENTION
[0008] It is, therefore, an object of the invention to provide an in-mold coating composition
having an excellent adhesion to SMC (sheet molding compound), BMC (bulk molding compound)
or a thermosetting molding resin having dicyclopentadiene as a main component, or
a thermoplastic molding resin such as ABS resin, polyamide resin, PPE resin, PC/PET,
PC/PBT or PC/ABS alloy, or the like, and an in-mold-coated molded product formed by
coating effectively with a white conductive coating film in a mold.
MEANS OF SOLVING THE PROBLEMS
[0009] The inventors have made various studies in order to solve the above-mentioned problems
and discovered that the above object can be achieved by the following constitutions,
and as a result the invention has been accomplished.
[0010] That is to say, according to the invention, there is provided an in-mold coating
composition characterized by comprising the following components:
- (A) at least one selected from a urethane oligomer, an epoxy oligomer, a polyester
oligomer and a polyether oligomer each having a (meth)acryloyl group, or an unsaturated
polyester resin,
- (B) a monomer capable of copolymerizing with the (A) component,
- (C) a conductive particle formed by coating a surface of an inorganic particle with
a conductive metal oxide particle, and
- (D) an organic peroxide polymerization initiator, wherein
mass ratios of the (A) and (B) components satisfy (A)/(B) = 20/80-80/20,
a mass ratio of the (C) component satisfies (C)/{(A)+(B)} = 5/100-50/100, and
a mass ratio of the (D) component satisfies (D)/{(A)+(B)} = 0.1/100-5/100.
[0011] According to the invention, there is also provided an in-mold-coated molded product
characterized by being produced, with any one of an injection molding method, an injection
compression molding method, an injection press molding method, a compression molding
method or a reaction injection molding method as a molding method, by the following
steps of:
clamping a mold composed of a fixed mold portion and a movable mold portion,
molding a resin in a cavity of the mold,
injecting an in-mold coating composition in the cavity,
curing the injected in-mold coating composition, and
removing a coated molded product after the curing of the in-mold coating composition,
wherein the in-mold coating composition is the above-mentioned in-mold coating composition.
EFFECTS OF THE INVENTION
[0012] According to the invention, there can be provided an in-mold-coated molded product
having a light-colored conductive coating film with an excellent adhesion by curing
an in-mold coating composition on the surface of a molded product of a thermosetting
molding resin or a thermoplastic molding resin in a mold, so that brighter color development
of the top coating film can be achieved by the subsequent electrostatic top coating.
Also, it is able to transfer the surface of a mold accurately by an in-mold coating
molding method, and it is able to effectively-reduce a sink mark or a weld line occurring
in a rib or a boss portion and accompanying the shrinkage of a molding resin which
is unsolvable in a usual coating.
BRIEF DESCRIPTION OF THE DRAWINGS
[0013]
FIG. 1 is a schematic configuration diagram showing an embodiment for forming an in-mold-coated
molded product according to the invention by means of a compression molding method.
FIG. 2 is a schematic configuration diagram showing an embodiment for forming an in-mold-coated
molded product according to the invention by means of an injection molding method
for a thermoplastic resin molding material.
FIG. 3 is a schematic configuration diagram showing an embodiment for forming an in-mold-coated
molded product according to the invention by means of a RIM method.
MODE FOR CARRYING OUT THE INVENTION
[0014] The in-mold-coated molded product according to the invention will be described concretely
below.
[0015] The in-mold-coated molded product according to the invention consists of a molded
product composed of a thermosetting molding resin or a thermoplastic molding resin
and a coating film of an in-mold coating composition formed on the surface thereof.
[0016] As the thermosetting molding resin may be used molding materials known heretofore,
and mentioned, for example, a fiber-reinforced plastic molding material, referred
to as SMC or BMC, containing an unsaturated polyester resin, an epoxy acrylate resin
or a phenol resin as a matrix, an RTM molding material containing an unsaturated polyester
resin, an epoxy acrylate resin or an epoxy resin as a matrix, a RIM molding material
using dicyclopentadiene, urethane or the like, and so on.
[0017] As the thermoplastic molding resin may be used various molding materials known heretofore,
and mentioned, for example, polycarbonate, polymethyl methacrylate, polystyrene, polyamide,
polyethylene terephthalate, polybutylene terephthalate, polyphenylene ether, ABS resin,
or an alloy material thereof.
[0018] Such molding materials may include, for example, a reinforcing agent such as glass
fiber, carbon fiber, calcium carbonate whisker or the like, an ultraviolet absorbing
agent, an antioxidant, a release agent, or the like so as to satisfy characteristics
depending on a use application.
[0019] Next, the in-mold coating material used in the invention will be described.
[0020] The in-mold coating material used in the invention comprises the following essential
components:
- (A) at least one selected from a urethane oligomer, an epoxy oligomer, a polyester
oligomer and a polyether oligomer each having a (meth)acryloyl group, or an unsaturated
polyester resin,
- (B) a monomer capable of copolymerizing with the (A) component,
- (C) a conductive particle formed by coating a surface of an inorganic particle with
a conductive metal oxide particle, and
- (D) an organic peroxide polymerization initiator, wherein
mass ratios of the (A) and (B) components satisfy (A)/(B) = 20/80-80/20,
a mass ratio of the (C) component satisfies (C)/{(A)+(B)} = 5/100-50/100, and
a mass ratio of the (D) component satisfies (D)/{(A)+(B)} = 0.1/100-5/100. As necessary,
the in-mold coating material used in the invention further comprises an optional component
such as an inorganic particle, such as calcium carbonate, talc or the like, having
an average particle diameter of not less than 0.1 µm but not more than 20 µm, a coloring
pigment such as titanium dioxide or the like, a low-shrinking agent such as a diallyl
phthalate oligomer, a saturated polyester resin or a polyvinyl acetate resin, a polymethyl
methacrylate resin or the like, a release agent, an ultraviolet absorbing agent, an
antioxidant, an anti-foaming agent, an antistatic agent, a polymerization inhibitor,
a curing accelerator, or the like.
(a) As to (A) component
[0021] The (A) component used in the in-mold coating composition used in the invention is
at least one selected from a urethane oligomer, an epoxy oligomer, a polyester oligomer
and a polyether oligomer each having a (meth)acryloyl group, or an unsaturated polyester
resin.
(a-1) Oligomer having a (meth)acryloyl group
[0022] The oligomer having the (meth)acryloyl group can include, for example, urethane (meth)acrylate,
polyester (meth)acrylate, epoxy (meth)acrylate and polyether (meth)acrylate.
[0023] The mass average molecular weights of these oligomers may vary depending on their
types, and are generally suitable to be about 300-30,000, preferably 500-10,000. The
oligomer having the (meth)acryloyl group is suitable to have a (meth)acryloyl group
of at least 2-8, preferably 2-6 in one molecular.
(a-1-1) Urethane (meth)acrylate oligomer
[0024] The urethane (meth)acrylate oligomer as a oligomer used in the invention can be produced
with a usual method, for example, by mixing (1) an organic diisocyanate compound,
(2) an organic polyol compound and (3) hydroxyalkyl (meth)acrylate at an abundance
ratio such that NCO/OH ratio is, for example, 0.8-1.0, preferably 0.9-1.0. When the
hydroxyl group is present in excess, or when hydroxyalkyl (meth)acrylate is used in
large amounts, an oligomer having a lot of hydroxyl groups is obtained.
[0025] Concretely, (1) the organic diisocyanate compound is reacted with (2) the organic
polyol compound or the like, for example, in the presence of a catalyst for urethane
reaction such as dibutyltin laurate or the like to obtain an isocyanate-terminated
polyurethane prepolymer. Then, the urethane (meth)acrylate oligomer can be produced
by reacting (3) hydroxyalkyl (meth)acrylate until reaction with a free isocyanate
group is mostly completed. With respect to ratio of (2) organic polyol compound and
(3) hydroxyalkyl (meth)acrylate, the amount of the former is suitable, for example,
to be about 0.1-0.5 moles based on 1 mole of the latter.
[0026] As (1) the organic diisocyanate compound used in the reaction can be used, for example,
1,2-diisocyanatoethane, 1,2-diisocyanatopropane, 1,3-diisocyanatopropane, hexamethylene
diisocyanate, lysine diisocyanate, trimethylhexamethylene diisocyanate, tetramethylene
diisocyanate, bis(4-isocyanatocyclohexyl)methane, methylcyclohexane-2,4-diisocyanate,
methylcyclohexane-2,6-diisocyanate, 1,3 -bis(isocyanatomethyl)cyclohexane, 1,3-bis(isocyanatoethyl)cyclohexane,
1,3-bis(isocyanatomethyl)benzene, 1,3-bis(isocyanato-1-methylethyl)benzene or the
like. These organic diisocyanate compounds can be used alone or as a mixture of two
or more.
[0027] As (2) the organic polyol compound used in the reaction can preferably be mentioned
organic diol compounds, for example, alkyldiol, polyether diol, polyester diol and
so on. As a representative example of the alkyldiol can be mentioned, for example,
ethylene glycol, 1,3-propanediol, propylene glycol, 2,3-butanediol, 1,4-butanediol,
2-ethylbutane-1,4-diol, 1,5-pentanediol, 1,6-hexanediol, 1,7-heptanediol, 1,8-octanediol,
1,9-nonanediol, 1,4-cyclohexanediol, 1,4-dimethylolcyclohexane, 4,8-dihydroxytricyclo[5.2.1.0
2,6]decane, 2,2-bis(4-hydroxycyclohexyl)propane and so on.
[0028] Polyether diol which is an organic diol compound can be synthesized, for example,
by polymerizing aldehyde, alkylene oxide, glycol or the like according to a known
method.
[0029] For example, polyether diol is obtained by an addition polymerization of formaldehyde,
ethylene oxide, propylene oxide, tetramethylene oxide, epichlorohydrin or the like
to alkyldiol under a suitable condition. As the polyester diol which is the organic
diol compound can be used, for example, an esterification reaction product obtained
by reacting a saturated or unsaturated dicarboxylic acid and/or an acid anhydride
thereof with an excess amount of alkyldiol, and an esterification reaction product
obtained by polymerizing hydroxycarboxylic acid and/or lactone as an intramolecular
ester thereof and/or lactide as an intermolecular ester thereof to alkyldiol. These
organic polyol compounds can be used alone or in a combination of two or more.
[0030] As (3) the hydroxyalkyl (meth)acrylate can be mentioned 2-hydroxyethyl (meth)acrylate,
2-hydroxypropyl (meth)acrylate, 4-hydroxybutyl (meth)acrylate, and so on. And, the
urethane (meth)acrylate oligomer as an oligomer used in the invention can be also
produced by reacting a compound having a (meth)acryloyl group and a hydroxyl group
in one molecule with an organic diisocyanate compound at NCO/OH ratio of, for example,
0.9-1.0 and, for example in the presence of a catalyst for urethane reaction such
as dibutyltin dilaurate or the like.
(a-1-2) Polyester (meth)acrylate oligomer
[0031] Polyester (meth)acrylate which is an oligomer used in the invention can be produced,
for example, by reacting polyester polyol having a hydroxyl group at its terminus
with an unsaturated carboxylic acid. Such polyester polyol can be produced representatively
by an esterification reaction of a saturated or unsaturated dicarboxylic acid or an
acid anhydride thereof with an excess of alkylene diol. As a representative example
of dicarboxylic acid used can be mentioned, for example, oxalic acid, succinic acid,
adipic acid, phthalic acid, maleic acid and so on. As a representative example of
alkylene diol used can be mentioned, for example, ethylene glycol, propylene glycol,
butanediol, pentanediol and so on. As a representative example of the unsaturated
carboxylic acid can be mentioned, for example, acrylic acid, methacrylic acid and
so on.
(a-1-3) Epoxy (meth)acrylate oligomer
[0032] Epoxy (meth)acrylate oligomer which is an oligomer used in the invention is produced,
for example, by using an epoxy compound and the above-mentioned unsaturated carboxylic
acid at a ratio such that, for example, 0.5-1.5 equivalents of carboxyl group is based
on one equivalent of epoxy group, and conducting a usual ring-opening addition reaction
of acid to epoxy group. As the epoxy compound used here can be preferably mentioned,
for example, a bisphenol-A-type epoxy, a novolac-type phenolic epoxy and so on.
(a-1-4) Polyether (meth)acrylate oligomer
[0033] Polyether (meth)acrylate which is an oligomer used in the invention can be produced,
for example, by reacting polyether polyol such as polyethylene glycol, polypropylene
glycol or the like with the above-mentioned unsaturated carboxylic acid.
(a-2) Unsaturated polyester resin
[0034] On the other hand, the unsaturated polyester resin used as the (A) component can
be produced, for example, by reacting an organic polyol compound with an unsaturated
carboxylic acid through a known method and, if necessary, further reacting with a
saturated polycarboxylic acid. As a representative example of the organic polyol used
can be mentioned, for example, ethylene glycol, propylene glycol, triethylene glycol,
trimethylolpropane, glycerin, bisphenol-A and so on. As a representative example of
the unsaturated polycarboxylic acid used can be mentioned, for example, (anhydrous)
maleic acid, (anhydrous) fumaric acid, (anhydrous) itaconic acid and so on.
[0035] These (A) components may be used in a combination of the (meth)acryloyl group-containing
oligomer and the unsaturated polyester resin.
(b) As to (B) component
[0036] The (B) component used in the invention is an unsaturated monomer capable of copolymerizing
with the (A) component.
[0037] As a representative example of such an unsaturated monomer can be mentioned, for
example, styrene, α-methylstyrene, chlorostyrene, vinyl toluene, methyl (meth)acrylate,
ethyl (meth)acrylate, propyl (meth)acrylate, butyl (meth)acrylate, 2-ethylhexyl (meth)acrylate,
ethylene glycol (meth)acrylate, cyclohexyl (meth)acrylate, glycidyl (meth)acrylate,
tetrahydrofurfuryl (meth)acrylate, 2-hydroxyethyl (meth)acrylate, (meth)acrylic acid
amide, 2-acrylamide-2-methylpropane sulfonic acid, (meth)acrylic acid, β-(meth)acryloyloxyethyl
hydrogen phthalate, β-(meth)acryloyloxyethyl hydrogen succinate, N-vinyl-2-pyrolidone,
N-vinylcaprolactam, ethylene glycol di(meth)acrylate, tripropylene glycol di(meth)acrylate,
1,6-hexanediol di(meth)acrylate, isobornyl (meth)acrylate, dimethyloltricyclodecane
di(meth)acrylate, trimethylolpropane tri(meth)acrylate, triallyl isocyanurate and
so on.
[0038] An aliphatic (meth)acrylate monomer like tripropylene glycol diacrylate (TPGDA) and
1,6-hexanediol diacrylate (1,6-HDDA), a (meth)acrylate monomer having an aliphatic
structure like cyclohexyl methacrylate, trimethylolpropane triacrylate (TMPT) and
so on are preferable.
[0039] With respect to the (B) component, the unsaturated monomers may be used alone or
as a mixture thereof. When it comprises a monomer having one ethylenic double bond
in one molecule and a monomer having two or more ethylenic double bond in one molecule,
it is particularly preferable to raise the hardness of the formed coating film and
thereby become difficult to scratch. It is preferable that the monomer having one
ethylenic double bond in one molecule is styrene monomer and the content of styrene
monomer to {(A)+(B)} components satisfies (styrene monomer)/{(A)+(B)} = 0.2/100-5/100
in a mass ratio, because the pot life is lengthened significantly.
[0040] The mass ratios of the (A) and (B) components depend on types of compounds used as
(A) and (B) components and so on, but they usually satisfy (A)/(B) = 20/80-80/20,
more preferably 33/67-67/33. When it is within this range, the curing properties is
better and hence a robust cured coating film is obtained, and also the in-mold flow
properties of the coating composition is better and hence a uniform coating film is
obtained without inclusion of bubbles.
(c) As to (C) component
[0041] As the (C) component used in the invention can be mentioned a conductive particle
formed by coating the surface of an inorganic particle such as an acicular titanium
dioxide, a potassium titanate whisker, mica or the like with a conductive metal oxide
particle.
[0042] The inorganic particle coated with the conductive metal oxide particle in the (C)
component is preferable to be at least one selected from titanium dioxide, zinc oxide,
alumina, silica, alkali titanate, or mica.
[0043] The conductive metal oxide particle is preferable to be an acicular titanium dioxide,
a potassium titanate whisker or a squamous mica, coated with any one of tin oxide,
antimony-doped tin oxide or tin-doped indium oxide.
[0044] The antimony-doped tin oxide preferably contains 0.1-5% by mass of at least one of
phosphorous, aluminum or molybdenum in an oxide form.
[0045] The conductive particle (C) is more preferable to have an aspect ratio of 3-200 because
of developing the conductive properties of the cured coating film.
[0046] In particular, the mass ratio of the (C) component satisfies (C)/{(A)+(B)} = 5/100-50/100,
more preferably 7/100-30/100. The mass ratio of the (C) component is preferable to
be not less than 5/100, because the cured coating film has sufficient conductive properties
and hence an electrostatic top coating is carried out effectively. On the other hand,
the mass ratio of the (C) component is preferable to be not more than 50/100, because
the rising of viscosity can be suppressed within the limits and the in-mold flow properties
are appropriate.
(d) As to (D) component
[0047] The (D) component used in the invention is an organic peroxide polymerization initiator
used for generating a free radical and polymerizing the (A) and (B) components. It
is particularly preferable that the organic peroxide polymerization initiator contains
an organic peroxide polymerization initiator having a one-minute half-life temperature
of not less than 85°C but less than 95°C and an organic peroxide polymerization initiator
having a one-minute half-life temperature of not less than 95°C but less than 170°C.
[0048] The organic peroxide polymerization initiator having a one-minute half-life temperature
of not less than 85°C but less than 95°C includes, for example, isobutyryl peroxide,
1,1,3,3-tetramethylbutyl peroxyneodecanoate, α-cumyl peroxyneodecanoate, di-3-methoxybutyl
peroxydicarbonate, di-2-ethylhexyl peroxydicarbonate, bis(4-t-butylcyclohexyl) peroxydicarbonate,
di-isopropyl peroxydicarbonate and so on. Bis(4-t-butylcyclohexyl) peroxydicarbonate
is particularly preferable. As a representative example of the organic peroxide polymerization
initiator having a one-minute half-life temperature of not less than 95°C but less
than 170°C are mentioned organic peroxides such as t-butyl peroxybenzoate, t-butyl
peroxyisobutyrate, t-butyl peroxy2-ethylhexanoate, t-amyl peroxy2-ethylhexanoate,
t-butyl peroxyisopropylcarbonate, lauroyl peroxide, benzoyl peroxide and so on. t-Butyl
peroxybenzoate and t-amyl peroxy2-ethylhexanoate are particularly preferable.
[0049] The mass ratio of the organic peroxide polymerization initiator as the (D) component
satisfies (D)/{(A)+(B)} = 0.1/100-5/100, more preferably 0.5/100-3/100. When the compounding
ratio of the organic peroxide polymerization initiator as the (D) component is less
than 0.1/100, the reaction between (A) and (B) components is not successfully progressed
and the failure of curing is caused not to obtain a normal coating film. While, when
it exceeds 5/100, the pot life of the coating composition is shortened significantly.
(e) As to other components
[0050] The in-mold coating composition used in the invention can further comprise at least
one inorganic particle, such as calcium carbonate, talc or the like, having an average
particle diameter of not less than 0.1 µm but not more than 20 µm as needed. As such
an inorganic particle may be preferably mentioned, for example, calcium carbonate,
talc, barium sulfate, aluminum hydroxide, clay and so on. These inorganic particles
are compounded for purposes of dispersing a shrinkage stress associated with the curing
of coating film, improving an adhesion to a molded product, smoothing concave and
convex in surface, or improving the appearance of the surface of a molded product.
[0051] The in-mold coating composition used in the invention can further comprise at least
one coloring pigment as needed. The coloring pigment can be various coloring pigments
conventionally-used for a usual plastics or a coating material.
[0052] For example, titanium dioxide, zinc oxide or the like can be used as a white pigment,
and titanium yellow or the like can be used as a yellow pigment.
[0053] These light-colored coloring pigments are compounded for purposes of coloring the
cured coating film of the in-mold coating composition in white color or light color,
and developing an intended color even if coated with a light color-based top coating
material having a poor hiding power.
[0054] In the invention, a release agent can be optionally used in combination in order
to release a cured coating film smoothly from a mold. As the release agent can be
mentioned, for example, stearic acid, hydroxystearic acid, stearate such as zinc stearate,
aluminum stearate, magnesium stearate, calcium stearate or the like, soybean oil lecithin,
silicone oil, fatty acid ester, fatty acid alcohol dibasic acid esters, and so on.
The compounding amounts of these release agents are preferable to be, for example,
0.1-5 parts by mass, more preferably 0.2-2 parts by mass based on 100 parts by mass
in total of {(A)+(B)} components. When it is within this range, the effect of releasing
from a mold is preferably exercised.
[0055] In the invention, a modified resin can be compounded for purpose of improving an
adhesion to various resins for substrate. As the modified resin used for this purpose
can be mentioned, for example, chlorinated polyolefin, maleic acid-modified polyolefin,
acrylic oligomer, polyvinyl acetate, polymethyl methacrylate, allyl ester oligomer
and so on.
[0056] The in-mold coating composition used in the invention may be further compounded with
various additives such as an antistatic agent, an antioxidant, an ultraviolet absorbing
agent, a curing accelerator, a pigment dispersant, an anti-foaming agent, a plasticizer
or the like as needed.
<Production method of in-mold-coated molded product>
[0057] With respect to the production method of the in-mold-coated molded product according
to the invention, the constitution of a molding machine for carrying out it, a molding
tool and an injection equipment for a coating composition are described concretely
below with reference to Drawings, but these concrete molding machine, molding tool
and injection equipment for a coating composition are not intended as limitations
of the invention.
[0058] FIG. 1 shows an equipment for carrying out a compression molding method, for example,
using a glass fiber-reinforced thermosetting molding material referred to as SMC.
As the molding method can be used a conventional method of molding in a mold without
limitations, and preferably a method described in
JP-B-S55-9291 or
JP-A-S61-273921 can be used.
[0059] In the equipment shown in FIG. 1, an upper mold 1 and a lower mold 2 of a separable
mold are opposite molding tool members to each other. The upper mold 1 and the lower
mold 2 are fixed on a movable platen 3 and a fixed platen 4 of a clamping equipment,
respectively. The movable platen 3 is constituted to move back and forth by a clamping
cylinder 5. A mold cavity 6 of a desired shape can be formed by the upper mold 1 and
the lower mold 2, and the cavity can be extended in a direction of an in-mold molded
product surface coated in the mold by the movement of the upper mold 1. The surface
coated in the mold may be one surface or two or more surfaces, and thus the extension
of the cavity in the direction of the surface coated in the mold may be one direction
or two or more direction. The glass fiber-reinforced plastic molding material is injected
between the upper mold 1 and the lower mold 2, and the clamping cylinder 5 is operated
to approximate the upper mold 1 to the lower mold 2, and hence the molding material
is formed into the shape of the cavity, and cured by applying a clamping pressure.
[0060] Also, the equipment shown in FIG. 1 is provided with an injector 7 comprising a shutoff
pin 7A as a means of injecting an in-mold coating composition, a measuring cylinder
8 for supplying a predetermined amount of an in-mold coating composition to the injector
7, and a supply pump 9 for supplying the in-mold coating composition from its storage
portion 10 to the measuring cylinder 8. At this moment, the measuring cylinder 8 is
provided with a plunger regulator 8A for injection of an in-mold coating composition.
[0061] In the molding, the clamping cylinder 5 is firstly operated to separate the upper
mold 1 from the lower mold 2, and the glass fiber-reinforced plastic molding material
is placed on the lower mold 2, and thereafter the clamping cylinder 5 is operated
to approximate the upper mold 1 to the lower mold 2 and hence the molding material
is formed into the shape of the cavity, and subjected to an application of a clamping
pressure. The clamping pressure is usually 4-15 MPa. The molding temperature is determined
optionally depending on a molding time, a kind of a molding material, and so on, but
it is usually suitable to be 120-180°C. It is desirable that a mold is previously
set to the above-mentioned temperature before a molding material is injected, and
the temperature is held until a cured coating film to be hereinafter described is
obtained.
[0062] Then, in the stage wherein the molded product in the cavity is cured to the extent
that it can withstand the injection and flow pressures of the in-mold coating composition,
the in-mold coating composition is injected from the injector 7 between the inner
wall of the upper mold 1 and the molded product surface coated in the mold in the
amount such that a cured coating film of a desired film thickness or preferably having
a film thickness of 20-1,000 µm can be obtained, while holding the clamping pressure
as it is, or after reducing the clamping pressure, or after separating the upper mold
1 from the surface of the molded product by a distance which is larger than the desired
film thickness of the cured coating film but does not disengage the fitting of the
upper mold 1 and the lower mold 2 or preferably by a distance of 0.2-5 mm.
[0063] After the injection of the in-mold coating composition, an injection port is closed
by the shutoff pin 7A, and the in-mold coating composition is cured on the surface
of the molded product in the cavity 6, if necessary, by moving the clamping cylinder
5 to conduct an clamping operation. The pressure is usually (re)applied to about 1-10
MPa so that the in-mold coating composition can uniformly coat the surface of the
molded product, and then usually held for about 10-300 seconds until a cured coating
film is formed. The cured coating film is thus formed on the surface of the molded
product, and thereafter the clamping cylinder 5 is operated to separate the upper
mold 1 from the lower mold 2 and the molded product having the cured coating film
is removed from the mold.
[0064] FIG. 2 shows an embodiment in the case of an injection molding method for a thermoplastic
resin molding material. In FIG. 2, reference sign 11 is a fixed platen of a clamping
equipment of an injection molding machine and reference sign 12 is a movable platen,
and they are provided with a fixed mold member 13 and a movable mold member 14, respectively,
which are opposite molding tool members to each other. The movable platen 12 is constituted
to move back and forth by a clamping cylinder 15. A cavity 16 of a desired shape is
formed in a fitting portion of the fixed mold member 13 and the movable mold member
14, and a thermoplastic resin molding material in a molten or softened state is injected
in the cavity 16, filled and set. When a molten resin molding material is injected
and filled, the cavity 16 is constituted to be able to inject the resin molding material
from an injection cylinder 17 having a screw through a nozzle 18 and a sprue 19. In
FIG. 2, reference sign 20 is a rib portion (boss portion) and reference sign 21 is
an ejector pin in releasing.
[0065] Also, a means of injecting an in-mold coating composition in FIG. 2 comprises an
injector 22 with a shutoff pin 22A, a measuring cylinder 23 for supplying a predetermined
amount of an in-mold coating composition to the injector 22, and a supply pump 25
for supplying the in-mold coating composition from its storage portion 24 to the measuring
cylinder 23. At this moment, the measuring cylinder 23 is provided with a plunger
regulator 23A for injection of an in-mold coating composition.
[0066] In the molding, the clamping cylinder 15 is firstly operated to close the fixed mold
member 13 and the movable mold member 14 and apply a clamping pressure. The clamping
pressure is required to be able to withstand the injection pressure of the resin molding
material. The injection pressure is usually a high pressure of 40-250 MPa in the portion
of the nozzle 18. In this process, the supply pump is operated to supply a required
amount of an in-mold coating composition to the measuring cylinder 23.
[0067] Then, the resin molding material in a molten or softened state is injected from the
injection cylinder 17 into the cavity 16 through the nozzle 17 and the sprue 19. In
the stage wherein the resin molding material is set in the mold to the extent that
it can withstand the injection and flow pressures of the in-mold coating composition,
the clamping pressure is reduced, or the movable mold portion 14 is moved back by
a distance which is larger than the following desired film thickness of the cured
coating film but does not disengage the fitting of the fixed mold member 13 and the
movable mold member 14 or preferably by a distance of 0.2-5 mm. Then, the shutoff
pin 22A is operated to open the injection port of the injector 22. Then, the plunger
regulator 23A for injection of an in-mold coating composition of the measuring cylinder
23 is operated to inject the in-mold coating composition in the cavity 16, i.e. between
the inner wall of the fixed mold member 13 and the molded resin product surface coated
in the mold, in the amount such that a cured coating film of a desired film thickness
or preferably having a film thickness of 20-1,000 µm can be obtained.
[0068] After the injection of the in-mold coating composition, the injection port is closed
again by the shutoff pin 22A and, if necessary, the clamping cylinder 15 is moved
to conduct an clamping operation, and the in-mold coating composition is pushed out
to coat the surface of the molded product in the mold, and the in-mold coating composition
is cured on the surface of the molded product in the cavity 16. Then, the clamping
cylinder 15 is operated to separate the movable mold member 14 from the fixed mold
member 13 and the molded product having the cured coating film is removed from the
mold.
[0069] FIG. 3 shows an embodiment in the case of a RIM molding method for a urethane or
dicyclopentadiene molding material. In Fig. 3, reference signs 26 and 27 are opposite
molding tool members to each other.
[0070] The molding tool members 26 (fixed type) and 27 (movable type) are fixed on a fixed
platen and a movable platen of a clamping equipment, respectively. The movable platen
is constituted to move back and forth by a clamping cylinder. The fixed platen, movable
platen and clamping cylinder of the clamping equipment are not shown in FIG. 3. A
cavity 28 of a desired shape is formed by both molding tool members 26 and 27, and
filled with a molding material containing dicyclopentadiene as a main component, which
is cured. When the molding material containing dicyclopentadiene as a main component
is filled, raw materials comprising as a main component an A liquid comprised of dicyclopentadiene
and a catalyst and a B liquid comprised of dicyclopentadiene and an activating agent
are temperature-modulated in storage tanks 29 and 30, respectively, and thereafter
the raw materials are mixed by raising a pressure to 50-200 bars with hydraulic cylinders
35 and 36 in measuring cylinders 31 and 32, and injecting them form opposite nozzles
in a mixing head 38 and impinging with each other.
[0071] On the other hand, the embodiment in FIG. 3 is provided with as a means of injecting
an in-mold coating composition an injector 39 comprising a shutoff pin 39A, an in-mold
coating composition-measuring cylinder 40 for supplying a predetermined amount of
an in-mold coating composition to the injector 39, and a supply pump 42 for supplying
the in-mold coating composition from its storage portion 41 to the measuring cylinder
40. At this moment, the measuring cylinder 40 is provided with a plunger regulator
40A for injection of an in-mold coating composition.
[0072] In the molding, the clamping cylinder is firstly operated to close the mold (molding
tool members 26 and 27) and apply a clamping pressure. The clamping pressure is usually
0.5-1 MPa. Then, the molding material containing dicyclopentadiene as a main component
is injected from the mixing head 38 into the cavity 28. In this process, the supply
pump 42 is operated to supply a required amount of an in-mold coating composition
to the measuring cylinder 40. In the stage wherein the molding material is properly
cured in the mold (to the extent that it can withstand the injection and flow pressures
of the in-mold coating composition), the clamping pressure is held as it is, or reduced.
Then, the injection port of the injector 39 is opened by movement of the shutoff pin
39A. Then, the plunger regulator 40A for injection of an in-mold coating composition
of the measuring cylinder 40 is operated to fill the cavity 28, i.e. a space between
the inner wall of the mold member 26 and the molded product surface, with the in-mold
coating composition.
[0073] After the shutoff pin 39A is closed again, the in-mold coating composition is cured
in the mold, if necessary, by moving the clamping cylinder to conduct a clamping operation.
Then, the clamping cylinder is operated to separate both tool members 26 and 27 and
the coated molded product is removed from the mold.
EXAMPLES
[0074] The invention will be described in more detail on the basis of the following Examples
and Comparative Examples, but they are not intended as limitations of the invention.
<Synthesis of urethane oligomer>
[0075] A urethane oligomer can be produced by polymerizing according to various known methods.
The synthesis example is as follows: dibutyltin dilaurate is charged into the amount
of (A) component shown in Table 1, in which the amount of dibtutyltin dilaurate charged
is 0.02 parts by mass based on 100 parts by mass in total of (A)-(C) components. Then,
the amount of (B) component shown in Table 1 is added dropwise thereto with holding
at 40°C and reacted for a sufficient time, and thereafter a solution dissolving hydroquinone,
in which the amount of hydroquinone dissolved is 0.1 parts by mass based on 100 parts
by mass in total of (A)-(C) components, is added dropwise to (C) component shown in
Table 1, and further stirred with heating at 75°C for a sufficient time. Thus, urethane
oligomers UAC-1-UAC-3 are obtained.
[0076]
Table 1
|
(A) |
(B) |
(C) |
Diisocyanate compound |
Diol compound |
Hydroxy group-containing (meth)acrylate |
Type |
Parts by mass |
Type |
Parts by mass |
Type |
Parts by mass |
UAC-1 |
(A-1) |
349 |
(B-1) |
1000 |
(C-1) |
273 |
UAC-2 |
(A-2) |
840 |
(B-2) |
1000 |
(C-2) |
607 |
UAC-3 |
(A-3) |
500 |
(B-3) |
1000 |
(C-1) |
273 |
(A-1) 2,4- and 2,6-toluene diisocyanates
(A-2) Isophorone diisocyanate
(A-3) Bis(4-isocyanatophenyl)methane
(B-1) Polypropylene glycol (average molecular weight of 1000)
(B-2) Polycaprolactone diol (average molecular weight of 500)
(B-3) Adduct of ethylene oxide with 2,2-bis(4-hydroxyphenyl) (average molecular weight
of 1000)
(C-1) 2-hydroxyethyl methacrylate
(C-2) Pentaerythritol triacrylate |
<Synthesis of epoxy oligomer>
[0077] 1,000 parts by mass of an epoxy compound (trade name: EPIKOTE 828 (made by Yuka Shell
Epoxy Corporation)), 490 parts by mass of methacrylic acid, 3 parts by mass of triethylamine
and 0.01 parts by mass of hydroquinone are charged into a reactor, and reacted at
125°C for 3 hours to obtain an epoxy oligomer EAC-1.
<Production of conductive particle (C)>
[0078] A conductive particle (C) can be produced according to various known methods.
• Production of conductive particle EC-1
[0079] 100 g of a rutile-type titanium dioxide powder (trade name: R-310, made by Sakai
Chemical Industry CO., Ltd.) (97% or more of TiO
2, and average primary particle diameter of 0.20 µm) is dispersed in 0.3 liters of
pure water, to which 16 g of trichloroacetic aicd and 19 g of sodium trichloroacetate
are added as a pH buffer agent.
[0080] An acidic aqueous solution of hydrochloric acid containing 17 g of stannic chloride
and 2.5 g of antimony (III) chloride and an aqueous solution of sodium hydroxide (75
g/liter) are simultaneously added over 30 minutes while holding at 90°C, and hence
the coating with the coprecipitated hydroxide of tin oxide and antimony oxide is carried
out. Washing with water, filtering and drying are carried out, and thereafter sintering
at 550°C for 1 hour is carried out to obtain 110 g of a white powder (coating amount
of 10% by mass), which has a whiteness degree of 83 and a volume resistivity of 4
Ω·cm.
• Production of conductive particle EC-2
[0081] 100 g of a squamous fluorine mica powder (trade name: MK-100, made by Coop Chemical
Co., Ltd.) (whiteness degree of 95, average particle diameter of 2 µm, and aspect
ratio of 20-30) is dispersed in 0.3 liters of pure water, and held at 90°C, and added
with an acidic aqueous solution of hydrochloric acid containing 3.5 g of stannic chloride,
and thereafter an aqueous solution of sodium hydroxide (75 g/liter) is gradually added
dropwise thereto over 10 minutes so as to be pH of 2-4, and hence hydrolyzing is carried
out to form a coating film of tin hydrate on the powder.
[0082] Then, the solution is held at 90°C, to which an acidic aqueous solution of hydrochloric
acid containing 14 g of stannic chloride and 5 g of antimony (III) chloride and an
aqueous solution of sodium hydroxide (75 g/liter) are simultaneously added dropwise
over 30 minutes so as to be pH of 2-4, and hence the powder having the coating film
of tin hydrate is coated with the coprecipitated hydrate of tin and antimony. The
resulting powder is filtered, washed with water and dried, and thereafter sintered
at 550°C for 1 hour to obtain 111 g of a white powder (coating amount of 11 % by mass),
which has a whiteness degree of 83 and a volume resistivity of 370 Ω·cm.
• Production of conductive particle EC-3
[0083] 100 g of an acicular powder of rutile-type titanium dioxide (trade name: FTL-100,
made by Ishihara Sangyo Co., Ltd.) (fiber length of 1.68 µm, and fiber diameter of
0.13 µm) is dispersed in 0.3 liters of pure water, to which 16 g of trichloroacetic
aicd and 19 g of sodium trichloroacetate are added as a pH buffer agent.
An acidic aqueous solution of hydrochloric acid containing 17 g of stannic chloride
and 2.5 g of antimony (III) chloride and an aqueous solution of sodium hydroxide (75
g/liter) are simultaneously added over 30 minutes while holding at 90°C, and hence
the coating with the coprecipitated hydroxide of tin oxide and antimony oxide is carried
out. Washing with water, filtering and drying are carried out, and thereafter sintering
at 550°C for 1 hour is carried out to obtain 110 g of a white powder (coating amount
of 10% by mass), which has a whiteness degree of 88 and a volume resistivity of 6
Ω·cm.
• Production of conductive particle EC-4
[0084] 100 g of a rutile-type titanium dioxide powder (trade name: R-310, made by Sakai
Chemical Industry CO., Ltd.) (97% or more of TiO
2, and average primary particle diameter of 0.20 µm) is dispersed in 0.3 liters of
pure water, to which an acidic aqueous solution of hydrochloric acid containing 34
g of stannic chloride and 5 g of antimony trichloride and 50 milliliters of an aqueous
solution of sodium hydroxide (500 g/liter) containing 0.7 g of sodium hexametaphosphate
are simultaneously added dropwise over 30 minutes while holding at 90°C, whereby the
coating with the coprecipitated hydroxide of tin oxide and antimony oxide containing
phosphorus is carried out. Washing with water, filtering and drying are carried out,
and thereafter sintering at 600°C for 1 hour is carried out to obtain 121 g of a white
powder (coating amount of 20% by mass, containing 1% by mass of phosphorus), which
has a whiteness degree of 87 and a volume resistivity of 7 Ω·cm.
• Production of conductive particle EC-5
[0085] A white powder is produced in the same manner as in the conductive particle EC-3
except that an aqueous solution of sodium hydroxide containing 0.3 g of sodium aluminate
is used. There is obtained 120 g of the white powder (coating amount of 20% by mass,
containing 0.8% by mass of aluminum), which has a whiteness degree of 86 and a volume
resistivity of 2 Ω·cm.
<Examples 1-4 and Comparative Examples 1-5>
[0086] A mold having a cavity for obtaining a molded resin product having a product shape
of 800 mm in length, 300 mm in width, 50 mm in height and 3 mm in board thickness
is used to conduct an in-mold coating to a molded product according to the embodiment
shown in FIG. 1. In this case, a mold temperature is set to 150°C in the upper mold
and 135°C in the lower mold. First of all, an SMC molding material is put on the lower
mold, and then clamped at a clamping pressure of 2400 KN and held for 80 seconds,
and cured to the extent that the surface of the obtained molded product of SMC can
withstand injection and flow pressures of an in-mold coating composition. Then, the
clamping pressure is reduced to 360 KN and thereafter each of in-mold coating compositions
of 36 cm
3 having the compositions shown in Table 3 is injected between the surface of the mold
and the surface of the molded product over about 1.5 seconds. After the completion
of injection, the clamping pressure is raised to 1440 KN over 1 second and held for
10 seconds and thereafter the clamping pressure is reduced to 960 KN and held for
80 seconds, whereby the in-mold coating composition is cured.
[0087] With respect to the resulting molded product, the appearance of the coating film,
the surface resistance value, the L* value based on L*a*b* display system prescribed
in JIS Z 8729 and the adhesion of the coating film to a substrate are measured. The
results are shown in Table 4.
[0088] Further, the resulting molded product is subjected to an electrostatic coating under
the condition shown in Table 2. The coat appearance after the top coating is evaluated.
DELICON #1500 white (made by Dai Nippon Toryo Co., Ltd.) is used as a top coating
material.
[0089]
Table 2
Items |
Setting value |
Remarks |
Gun distance (cm) |
32 |
|
Shaping air pressure (Kgf/cm2) |
2.5 |
|
Air motor pressure (Kgf/cm2) |
3.5 |
18000 rpm |
Discharge amount (cc/min) |
230 |
|
Applied voltage (kV) |
-90 |
|
Conveyor speed (m/min) |
4.6 |
|
[Appearance of coating film]
[0090] The gloss, flow streak, uniformity and so on of the coating film are visually confirmed,
and the appearance is evaluated according to the followings:
Good ··· Uniform gloss, no flow streak, and uniform appearance.
Average ··· A little unevenness of gloss and flow streak.
Bad ··· Severe unevenness of gloss and flow streak, and ununiform appearance.
[L* value]
[0091] L* value is measured on the basis of L*a*b* display system prescribed in JIS Z 8729.
[Surface resistance value]
[0092] The surface resistance value of the coating film is measured by using a measuring
apparatus of Hiresta-UP MCP-HT450 type (made by Mitsubishi Chemical Corporation),
after it is left in a room at 23±2°C and 50±5% RH for 24 hours.
[Adhesion of coating film to substrate]
[0093] The initial coat adhesion test is carried out according to JIS K 5600-5-6: Adhesion
(cross-cut method). The adhesion of coating film is rated on the following 6-point
scale of 0 to 5 based on the classification of test results described in JIS K 5600-5-6.
<6-point scale>
[0094]
0 ··· The cut edge is fully smooth, and peelings are not present in any squares of
the lattice.
1 ··· Small peelings of the coating film are present in the cut cross-point. The percentage
of the affected portions in the cross-cut portions does not certainly exceed 5%.
2 ··· The coating film peels along the cut edge and/or in the cut cross-point. The
percentage of the affected portions in the cross-cut portions certainly exceeds 5%,
but it does not exceed 15%.
3 ··· The coating film forms large peelings partially or fully along the cut edge,
and/or different portions in squares peel partially or fully. The percentage of the
affected portions in the cross-cut portions certainly exceeds 15%, but it does not
exceed 35%.
4 ··· The coating film forms large peelings partially or fully along the cut edge,
and/or several squares peel partially or fully. The percentage of the affected portions
in the cross-cut portions certainly exceeds 35%, but it does not exceed 65%.
5 ··· The degree of peelings exceeds the Classification 4.
[Coat appearance after top coating]
[0095]
Good ··· Invisible substrate, uniform gloss, and uniform appearance.
Bad ··· Visible substrate, uneven gloss, and ununiform appearance.
[0097]

<Examples 5 and 6>
[0098] A mold having a cavity for obtaining a molded resin product having a box shape of
300 mm in length, 200 mm in width, 30 mm in height and 2.5 mm in board thickness is
used to conduct an in-mold coating to a molded product according to the embodiment
shown in FIG. 2. A mold temperature is set to 100°C in the fixed mold and 80°C in
the movable mold, and a barrel temperature is heated to 180°C. First of all, a rubber-modified
polypropylene resin is melted with heating in the injection cylinder, and then injected
into the mold clamped at a clamping pressure of 3,000 KN over about 1.5 seconds, and
then held at a pressure of 40 MPa for 5 seconds. It is cooled in the situation subjected
to the clamping pressure for 40 seconds, and solidified to the extent that the surface
of the obtained molded product can withstand injection and flow pressures of an in-mold
coating composition. Then, the movable mold is spaced about 0.5 mm apart, and thereafter
each coating composition shown in Table 5 of 9 cm
3 is injected between the surface of the mold and the surface of the molded product
over about 0.5 seconds. After the completion of injection, the clamping pressure is
raised to 200 KN over 1 second and held for 120 seconds, whereby the in-mold coating
composition is cured.
[0099]
Table 5
|
Example 5 |
Example 6 |
(A) |
UAC-2 |
20.0 |
20.0 |
(B) |
HDDA |
30.0 |
30.0 |
DCPA |
10.0 |
10.0 |
(C) |
EC-3 |
15.0 |
15.0 |
(D) |
Bis(4-t-butylcyclohexyl) peroxydicarbonate |
1.0 |
1.0 |
Release agent |
Zinc stearate |
0.3 |
0.3 |
ZELEC-NE |
0.2 |
0.2 |
Inorganic particle |
Talc |
5.0 |
|
Coloring pigment |
Titanium dioxide |
|
5.0 |
Modified resin |
Superchlon 822S |
30.0 |
30.0 |
|
Adekastab NA-11 |
|
0.3 |
Plasticizer |
TXIB |
1.0 |
1.0 |
(A)/(B) |
33.3/66.7 |
33.3/66.7 |
(C)/(A)+(B) |
25/100 |
25/100 |
(D)/(A)+(B) |
1.7/100 |
1.7/100 |
HDDA: 1,6-hexanediol diacrylate.
DCPA: dimethyloltricyclodecane diacrylate.
ZELEC-NE: neutralized alcohol phosphate (made by DuPont Corporation).
Superchlon 822S: chlorinated polyolefin (made by Nippon Paper Corporation).
Adekastab NA-11: a metal salt of a phosphoric acid ester (made by Asahi Denka Corporation).
TXIB: 2,2,4-trimethy-1,8-pentanediol diisobutylate |
[0100] With respect to the resulting molded product, the appearance of the coating film,
the surface resistance value, the L* value based on L*a*b* display system prescribed
in JIS Z 8729 and the adhesion of the coating film to a substrate are measured in
the same manner as in the above Examples. The results are shown in Table 6.
[0101] Further, the resulting molded product is subjected to an electrostatic coating under
the same condition as described above. The coat appearance after the top coating is
evaluated. In this case, PLANITTO#3600PA white (made by Dai Nippon Toryo Co., Ltd.)
is used as a top coating material.
[0102]
Table 6
|
Example 5 |
Example 6 |
Appearance of coating film |
Good |
Good |
L* value |
81.1 |
90.5 |
Surface resistance value [Ω/□] |
1.0×105 |
2.3×106 |
Adhesion of coating film to substrate |
0 |
0 |
Coat appearance after top coating |
Good |
Good |
<Examples 7-13 and Comparative Examples 6-8>
[0103] A mold having a cavity for obtaining a molded resin product having a box shape of
300 mm in length, 200 mm in width, 30 mm in height and 2.5 mm in board thickness is
used to conduct an in-mold coating to a molded product according to the embodiment
shown in FIG. 2. A mold temperature is set to 95°C in the fixed mold and 75°C in the
movable mold, and a barrel temperature is heated to 200°C. First of all, an ABS resin
is melted with heating in the injection cylinder, and then injected into the mold
clamped at a clamping pressure of 3,500 KN over about 1 second, and cooled for 30
seconds, and set to the extent that the surface of the obtained molded product can
withstand injection and flow pressures of an in-mold coating composition.
[0104] Then, the movable mold is spaced about 1 mm apart, and thereafter each coating composition
shown in Table 7 of 13 cm
3 is injected between the surface of the mold and the surface of the molded product
over about 0.5 seconds. After the completion of injection, the clamping pressure is
raised to 200 KN over 1 second and held for 60 seconds, whereby the in-mold coating
composition is cured.
[0105]

[0106] With respect to the resulting molded product, the appearance of the coating film,
the surface resistance value, the L* value based on L*a*b* display system prescribed
in JIS Z 8729 and the adhesion of the coating film to a substrate are measured in
the same manner as in the above Examples. The results are shown in Table 8.
[0107] Further, the resulting molded product is subjected to an electrostatic coating under
the same condition as described above. The coat appearance after the top coating is
evaluated. In this case, PLANITTO #3600PA white (made by Dai Nippon Toryo Co., Ltd.)
is used as a top coating material.
[0108]

<Examples 14-17 and Comparative Example 9>
[0109] A mold having a cavity for obtaining a molded resin product using dicyclopentadiene
as a main raw material and having a box shape of 400 mm in length, 400 mm in width
and 30 mm in height is used to conduct an in-mold coating to a molded product according
to the embodiment shown in FIG. 3. In this case, a mold temperature is set to 95°C
in the upper mold and 60°C in the lower mold. First of all, a molding material containing
dicyclopentadiene as a main raw material is injected into the mold clamped at a clamping
pressure of 160 KN, and then cured for 60 seconds
[0110] Then, each in-mold coating composition shown in Table 9 of 32 cm
3 is injected between the surface of the mold and the surface of the molded product
over about 1 second, while holding the clamping pressure. After the completion of
injection, it is held for 200 seconds, whereby the in-mold coating composition is
cured.
[0111]
Table 9
|
Examples |
Comparative Example |
Example 14 |
Example 15 |
Example 16 |
Example 17 |
Comparative Example 9 |
(A) |
UAC-2 |
30.0 |
20.0 |
30.0 |
30.0 |
31.0 |
UAC-3 |
--- |
--- |
--- |
--- |
--- |
EAC-1 |
--- |
10.0 |
--- |
--- |
--- |
(B) |
TPGDA |
45.0 |
45.0 |
44.0 |
45.0 |
46.5 |
Styrene |
--- |
--- |
1.0 |
--- |
--- |
(C) |
EC-3 |
15.0 |
15.0 |
15.0 |
15.0 |
--- |
EC-5 |
--- |
--- |
--- |
--- |
--- |
(D) |
Bis(4-t-butylcyclohexyl) peroxydicarbonate |
1.0 |
1.0 |
0.8 |
0.8 |
1.0 |
t-Amyl peroxy2-ethylhexanoate |
--- |
--- |
0.4 |
0.4 |
--- |
Release agent |
Zinc stearate |
0.8 |
0.8 |
0.8 |
0.8 |
0.8 |
Conductive material |
Ketjen black EC600 |
--- |
--- |
--- |
--- |
4.0 |
Inorganic particle |
Talc |
10.0 |
10.0 |
10.0 |
10.0 |
10.0 |
Plasticizer |
TXIB |
1.0 |
1.0 |
0.8 |
0.8 |
1.0 |
(A)/(B) |
40/60 |
40/60 |
40/60 |
40/60 |
40/60 |
(C)/(A)+(B) |
20/100 |
20/100 |
20/100 |
20/100 |
0/100 |
(D)/(A)+(B) |
1.3/100 |
1.3/100 |
1.6/100 |
1.6/100 |
1.3/100 |
[0112] With respect to the resulting molded product, the appearance of the coating film,
the surface resistance value, the L* value based on L*a*b* display system prescribed
in JIS Z 8729 and the adhesion of the coating film to a substrate are measured in
the same manner as in the above Examples. The results are shown in Table 10.
[0113] Further, the resulting molded product is subjected to an electrostatic coating under
the same condition as described above. The coat appearance after the top coating is
evaluated. In this case, PLANITTO#3600PA white (made by Dai Nippon Toryo Co., Ltd.)
is used as a top coating material.
[0114]
Table 10
|
Examples |
Comparative Example |
Example 14 |
Example 15 |
Example 16 |
Example 17 |
Comparative Example 9 |
Appearance of coating film |
Good |
Good |
Good |
Good |
Bad |
L* value |
82.3 |
91.9 |
82.1 |
82.8 |
15.5 |
Surface resistance value [Ω/□] |
1.7×106 |
3.9×106 |
2.5×106 |
1.1×106 |
4.5×104 |
Adhesion of coating film to substrate |
1 |
1 |
1 |
1 |
5 |
Coat appearance after top coating |
Good |
Good |
Good |
Good |
Bad |